A process of producing an organic compound and/or an intermediary compound as defined herein by feeding carbon dioxide to a culture of a cyanobacterial cell and subjecting the culture to light, wherein the cell is capable of expressing a nucleic acid molecule, wherein the expression of the nucleic acid molecule confer on the cell the ability to convert a glycolytic intermediate into the organic compound and/or into the intermediary compound and wherein the nucleic acid molecule is under the control of a regulatory system which responds to a change in the concentration of a nutrient in the culture.

Patent
   9228210
Priority
Dec 17 2007
Filed
Dec 17 2008
Issued
Jan 05 2016
Expiry
Jun 07 2031
Extension
902 days
Assg.orig
Entity
Small
0
20
currently ok
5. A cyanobacteria that expresses a nucleic acid molecule that allows the cyanobacteria to convert pyruvate into butanol, wherein,
the nucleic acid molecule is under the control of a regulatory system which responds to a change in the concentration of a nutrient when culturing said cyanobacteria, and
said nucleic acid molecule encodes one or more enzyme that converts pyruvate to butanol, the enzyme being selected from the group consisting of: 2-acetolactate synthetase, acetolactate decarboxylase, diacetyl reductase, acetoin reductase, glycerol dehydratase, and 1,3-propanediol dehydrogenase.
1. A process for producing butanol, comprising:
culturing cyanobacteria cells in culture medium;
feeding carbon dioxide to the cyanobacteria cells; and
subjecting the cyanobacteria cells to light,
wherein,
the cyanobacteria cells expresses a nucleic acid molecule that allows the cells to convert a pyruvate into said butanol,
the nucleic acid molecule is under control of a regulatory system which responds to a change in concentration of a nutrient when culturing said cyanobacteria cells, and
said nucleic acid molecule encodes one or more enzyme that converts pyruvate to butanol, said enzyme being selected from the group consisting of 2-acetolactate synthetase, acetolactate decarboxylase, diacetyl reductase, acetoin reductase, glycerol dehydratase, and 1,3-propanediol dehydrogenase.
8. A process for producing butanol, or for producing 2-acetolactate, acetoin, 2,3 butanediol or 2-butanone produced in a pathway leading to butanol, comprising:
culturing cyanobacteria cells in culture medium;
feeding carbon dioxide to the cyanobacteria cells; and
subjecting the cyanobacteria cells to light,
wherein,
the cyanobacteria cells express a nucleic acid molecule that allows the cells to convert pyruvate into said butanol, 2-acetolactate, acetoin, 2,3 butanediol or 2-butanone,
the nucleic acid molecule is under control of a regulatory system that responds to a change in concentration of a nutrient when culturing said cyanobacteria cells, and
said nucleic acid molecule encodes one or more enzyme that converts pyruvate to butanol, said enzyme being selected from the group consisting of 2-acetolactate synthetase, acetolactate decarboxylase, diacetyl reductase, acetoin reductase, glycerol dehydrase, and 1,3-propanediol dehydrogenase.
2. The process of claim 1, wherein said one or more enzyme is not sensitive towards oxygen inactivation.
3. The process of claim 1, wherein,
the regulatory system responds to a change in the concentration of the nutrient ammonium,
the nucleic acid molecule is integrated into the cell genome, and/or
the cyanobacteria cells are from the genus Synechocystis.
4. The process of claim 1, further comprising isolating the butanol produced in said process.
6. The cyanobacteria of claim 5, wherein,
the regulatory system responds to a change in the concentration of the nutrient ammonium,
the nucleic acid molecule is integrated into the cyanobacteria genome, and/or
the cyanobacteria is from the genus Synechocystis.
7. The process of claim 2, wherein,
the nucleic acid molecule encodes one or more enzyme that converts pyruvate to butanol, the enzyme being selected from the group consisting of 2-acetolactate synthetase, acetolactate decarboxylase, diacetyl reductase, acetoin reductase, glycerol dehydratase, and 1,3-propanediol dehydrogenase.
9. The process of claim 8, wherein,
the regulatory system responds to a change in the concentration of the nutrient ammonium,
the nucleic acid molecule is integrated into the cell genome, and/or
the cyanobacteria cells are from the genus Synechocystis.
10. The process of claim 8, further comprising isolating the butanol, 2-acetolactate, acetoin, 2,3 butanediol or 2-butanone produced in said process.
11. The process of claim 8, for producing butanol or for producing 2,3 butanediol in a pathway leading to butanol.
12. The process of claim 11, further comprising isolating the butanol or 2,3 butanediol produced in said process.
13. The process of claim 8, for producing butanol.
14. The process of claim 13, further comprising isolating the butanol produced in said process.

The invention relates to a process of producing an organic compound and/or an intermediary compound produced in the pathway leading to said organic compound by feeding carbon dioxide to a culture of a cyanobacterial cell and subjecting said culture to light, wherein said cell is capable of expressing a nucleic acid molecule wherein the expression of said nucleic acid molecule confers on said cell the ability to convert a glycolytic intermediate such as pyruvate or glyceraldehyde 3-phosphate into said organic compound and/or into said intermediary compound and wherein expression of said nucleic acid molecule is under the control of a regulatory system which responds to a change in the concentration of a nutrient in said culture. The invention further relates to a cyanobacterial cell for use in this process.

Our economy is driven by the use of fossil fuels. Shortages caused by exhausting oil supplies primarily affect the transport sector of our society and the chemical industry, but secondarily affect all aspects of human activities. As an additional problem, the use of oil supplies has caused the build-up of a high CO2 concentration in the atmosphere.

Energy ultimately comes from the sun and this energy drives photosynthetic process in plants and photoautotrophic bacteria. This knowledge has led to new methods for the synthesis of biofuels. In essence, these processes employ plants and algal species to reduce CO2 to the level of sugars and cell material. After harvesting, these end products are converted to ethanol by yeast fermentation (in the case of crops) or converted chemically to biofuels (in the case of algae). The overall energy conservation of these methods is highly inefficient and therefore demands large surface areas. In addition, the processes are rather labor-intensive, are demanding with respect to water consumption and affect foodstock prices with adverse consequences for food supplies. A more remotely similar process is based on the conversion of solar energy into hydrogen. Also this process suffers from a severely decreased efficiency.

Numerous biotechnological processes make use of genetically engineered organisms in order to produce bulk or fine chemicals, proteins or antibiotics. In many cases, increased production has been obtained by improved gene expression and by optimization of growth conditions. In all processes we are aware of, the initial carbon-precursor has been and still is sugar (notably glucose, but many other mono- and polysaccharides are in use) or related organic substrates: solventogenesis (including butanol and ethanol) and organic acid production (e.g. lactic-, citric- or succinic acid) always starts from glucose, which makes it inefficient as the production process uses a high energy initial compound as substrate.

U.S. Pat. No. 6,699,696 describes a process of producing ethanol by feeding carbon dioxide to a cyanobacterial cell, especially a Synechococcus comprising a nucleic acid molecule encoding an enzyme enabling the cell to convert pyruvate into ethanol, subjecting said cyanobacterial cell to sun energy and collecting ethanol. This system has several drawbacks among others the expression system used is temperature sensitive which demands to adapt the production system for such regulation.

Therefore, there is still a need for an alternative and even improved production process of an organic compound, which do not have all the drawbacks of existing processes.

The present invention relates to a scalable process for the production of an organic compound suitable as chemical feedstock or as a biofuel. The invention combines metabolic properties of photoautotrophic and chemoorganotrophic prokaryotes and is based on the employment of recombinant oxyphototrophs with high rates of conversion of Calvin cycle intermediates to a fermentative end product. Its novelty resides in the fact a) that its core chemical reactions use CO2 as the sole carbon-containing precursor and light (preferably sunlight) as the sole energy source to drive CO2 reduction and b) that a great variety of end products can be realized by the same principle, namely introduction of a nucleic acid molecule cassette encoding a specific fermentative pathway and c) that production is controlled by a medium component and starts at the most appropriate time, namely at the highest possible cell density. Whereas in current applications of fuel production, organisms are substrate (crops in ethanol production) or product (microalgae as biodiesel), here microorganisms are used as highly specialized catalysts for the conversion of CO2 as substrate to a useful end product. These catalysts can be subjected to optimization strategies through physical- and chemical systems-biology approaches. The biochemical background of the invention is more extensively described in example 1. Each aspect of the invention is more extensively described below.

Cyanobacteria

In a first aspect, the invention provides a Cyanobacteria capable of expressing a nucleic acid molecule, wherein the expression of said nucleic acid molecule confers on the Cyanobacteria the ability to convert a glycolytic intermediate into an organic compound and/or into an intermediary compound produced in the pathway leading to said organic compound and wherein the nucleic acid molecule is under the control of a regulatory system which responds to a change in the concentration of a nutrient when culturing said Cyanobacteria.

In the context of the invention a Cyanobacterium or a cyanobacterial cell is a blue-green algae which is a photosynthetic unicellular prokaryote. Examples of Cyanobacteria include the genera Aphanocapsa, Anabaena, Nostoc, Oscillatoria, Synechococcus, Gloeocapsa, Agmenellum, Scytonema, Mastigocladus, Arthrosprira, Haplosiphon. A preferred genus is Synechococcus. A more preferred species of this genus is a Synechocystis species. Even more preferably, the Synechocystis is a Pasteur Culture Collection (PCC) 6083 Synechocystis, which is a publicly available strain via ATCC for example. A preferred organism used is the phototrophic Synechocystis PCC 6083: this is a fast growing cyanobacterium with no specific nutritional demands. Its physiological traits are well-documented: it is able to survive and grow in a wide range of conditions. For example, Synechocystis sp. PCC 6803 can grow in the absence of photosynthesis if a suitable fixed-carbon source such as glucose is provided. Perhaps most significantly, Synechocystis sp. PCC 6803 was the first photosynthetic organism for which the entire genome sequence was determined. In addition, an efficient gene deletion strategy (Shestakov SV et al, (2002), Photosynthesis Research, 73: 279-284 and Nakamura Y et al, (1999), Nucleic Acids Res. 27:66-68) is available for Synechocystis sp. PCC 6803, and this organism is furthermore easily transformable via homologous recombination (Grigirieva GA et al, (1982), FEMS Microbiol. Lett. 13: 367-370).

A Cyanobacteria as defined herein is capable of converting a glycolytic intermediate into an organic compound and/or into an intermediary compound as defined herein. A biochemical background of the Cyanobacteria of the invention is given in Example 1.

A Cyanobacteria as defined herein preferably comprises a nucleic acid molecule encoding an enzyme capable of converting a glycolytic intermediate into an organic compound and/or into an intermediary compound as defined herein. An organic compound is herein preferably defined as being a compound being more reduced than CO2. A Cyanobacteria is therefore capable of expressing a nucleic acid molecule as defined herein, whereby the expression of a nucleic acid molecule as defined herein confers on the Cyanobacteria the ability to convert a glycolytic intermediate into an organic compound and/or into an intermediary compound all as defined herein. A glycolytic intermediate may be dihydroxyacetone-phosphate, glyceraldehyde-3-phosphate, 1,3-bis-phosphoglycerate, 2-phosphoglycerate, 3-phosphoglycerate, phospho-enol-pyruvate and pyruvate. Preferred glycolytic intermediates are pyruvate and glyceraldehyde-3-phosphate. The skilled person knows that the identity of the glycolytic intermediate converted into an organic product to be produced depends on the identity of the organic product to be produced.

Preferred organic products are selected from: a C1, C2, C3, C4, C5, or C6 alkanol, alkanediol, alkanone, alkene, or organic acid. Preferred alkanols are C2, C3 or C4 alkanols. More preferred are ethanol, propanol, butanol. A preferred alkanediol is 1,3-propanediol. A preferred alkanone is acetone. A preferred organic acid is D-lactate. A preferred alkene is ethylene.

A preferred glycolytic intermediate for the production of ethanol, propanol, butanol, acetone or D-lactate is pyruvate. A preferred glycolytic intermediate for the production of 1,3-propanediol is glyceraldehyde-3-phosphate. A preferred glycolytic intermediate for the production of ethylene is alpha-oxyglutarate

“Converting a glycolytic intermediate into an organic compound” preferably means that detectable amounts of an organic compound are detected in the culture of a Cyanobacteria as defined herein cultured in the presence of light and dissolved carbon dioxide and/or bicarbonate ions during at least 1 day using a suitable assay for the organic compound. A preferred concentration of said dissolved carbon dioxide and/or bicarbonate ions is at least the natural occurring concentration at neutral to alkaline conditions (pH 7 to 8) being approximately 1 mM. A more preferred concentration of carbon dioxide and/or bicarbonate ions is higher than this natural occurring concentration. A preferred method to increase the carbon dioxide and/or bicarbonate ions in solution is by enrichment with waste carbon dioxide from industrial plants. The concentration of carbon dioxide in the gas that is sparged into the culture broth may be increased from the equivalent of 0.03% (air) up to 0.2%.

In another preferred embodiment, a Cyanobacterium converts a glycolytic intermediate into an intermediary component of the pathway leading to a given organic compound. In this embodiment, detectable amounts of an intermediary compound are detected in a Cyanobacterium and/or in its culture, wherein said Cyanobacterium is cultured in the presence of sunlight and carbon dioxide during at least 1 day using a given assay for the intermediary compound. Depending on the identity of the organic compound, the skilled person will know which intermediary compound may be produced.

All organic compounds or intermediary compounds produced are produced within the cell and may spontaneously diffuse into the culture broth. A preferred assay for said intermediates and alkanols, alkanones, alkanediols and organic acids is High Performance Liquid Chromatography (HPLC). A detectable amount for said intermediates and alkanols, alkanones, alkanediols and organic acids is preferably at least 0.1 mM under said culture conditions and using said assay. Preferably, a detectable amount is at least 0.2 mM, 0.3 mM, 0.4 mM, or at least 0.5 mM.

Ethanol as Organic Compound

When an organic product to be produced is ethanol, preferred nucleic acid molecules code for enzymes capable of converting pyruvate into ethanol and/or into an intermediary compound produced in the pathway leading to ethanol, said enzymes comprise a pyruvate decarboxylase (pdc) and an alcohol dehydrogenase (adh). The intermediary compound is acetaldehyde. A preferred assay for acetaldehyde is HPLC. A detectable amount of acetaldehyde is preferably at least 0.1 mM under said culture conditions as defined earlier herein and using said assay. Therefore in this preferred embodiment, a Cyanobacterium comprises a nucleic acid molecule encoding a pdc and another one encoding an adh. Accordingly, this preferred embodiment relates to a Cyanobacterium capable of expressing the following nucleic acid molecules being represented by nucleotide sequences, wherein the expression of these nucleotide sequences confers on the cell the ability to convert pyruvate into acetaldehyde and/or into ethanol:

(a) a nucleotide sequence encoding a pdc, wherein said nucleotide sequence is selected from the group consisting of:

Propanol as Organic Compound

When an organic product to be produced is propanol, the preferred nucleic acid molecules code for enzymes capable of converting pyruvate into propanol and/or into an intermediary compound produced in the pathway leading to propanol, said enzymes comprise a thiolase, an acetoacetylCoA transferase, an acetoacetate decarboxylase and a propanol dehydrogenase. The intermediary compound is acetone. A preferred assay for acetone is HPLC. A detectable amount of acetone is preferably at least 0.1 mM under said culture conditions as defined earlier herein and using said assay. Therefore in this preferred embodiment, a Cyanobacterium comprises a nucleic acid molecule encoding a thiolase, an acetoacetylCoA transferase, an acetoacetate decarboxylase and another one encoding a propanol dehydrogenase. Accordingly, this preferred embodiment relates to a Cyanobacterium capable of expressing the following nucleic acid molecules being represented by nucleotide sequences, wherein the expression of these nucleotide sequences confers on the cell the ability to convert pyruvate into acetone and/or into propanol:

(a) a nucleotide sequence encoding a thiolase, wherein said nucleotide sequence is selected from the group consisting of:

A preferred acetoacetylCoA transferase is formed by two subunits: one is represented by SEQ ID NO:95, the other one by SEQ ID NO:96. Corresponding encoding nucleotide sequences are preferably represented by SEQ ID NO: 97, 98 respectively.

Butanol as Organic Product

Butanol is a preferred organic product. The invention encompasses at least two pathways for producing butanol.

In a first pathway, when an organic product to be produced is butanol, preferred nucleic acid molecules code for enzymes capable of converting pyruvate into butanol and/or into an intermediary compound produced in the pathway leading to butanol, said enzymes comprise a thiolase, a hydroxybutyrylCoA dehydrogenase, a crotonase, a butyryl-CoA dehydrogenase, a butyraldehyde dehydrogenase and a butanol dehydrogenase. A preferred intermediary compound is butyraldehyde. A preferred assay for butyraldehyde is HPLC. A detectable amount of butyraldehyde is at least 0.1 mM under said culture conditions as defined earlier herein and using said assay. Therefore in this preferred embodiment, a Cyanobacterium comprises a nucleic acid molecule encoding a thiolase, a hydroxybutyrylCoA dehydrogenase, a crotonase, a butyryl-CoA dehydrogenase, a butyraldehyde dehydrogenase and a butanol dehydrogenase. Accordingly, this preferred embodiment relates to a Cyanobacterium capable of expressing the following nucleotide molecules being represented by nucleotide sequences, wherein the expression of these nucleotide sequences confers on the cell the ability to convert pyruvate into butyraldehyde and/or into butanol:

(a) a nucleotide sequence encoding a thiolase, wherein said nucleotide sequence is selected from the group consisting of:

In a second pathway, when an organic product to be produced is butanol, preferred nucleic acid molecules code for enzymes capable of converting pyruvate into butanol and/or into an intermediary compound produced in the pathway leading to butanol, said enzymes comprise a 2-acetolactate synthetase, an acetolactate decarboxylase, a diacetyl reductase, an acetoin reductase, a glycerol dehydratase (a large, medium and small subunits thereof), a 1,3-propanediol dehydrogenase.

A preferred intermediary compound is 2,3-butanediol. A preferred assay for 2,3-butanediol is HPLC. A detectable amount of 2,3-butanediol is at least 0.1 mM under said culture conditions as defined earlier herein and using said assay. Therefore in this preferred embodiment, a Cyanobacterium comprises a nucleic acid molecule encoding a 2-acetolactate synthetase, an acetolactate decarboxylase, a diacetyl reductase, an acetoin reductase, a glycerol dehydratase (a large, medium and small subunits thereof), a 1,3-propanediol dehydrogenase.

Accordingly, this preferred embodiment relates to a Cyanobacterium capable of expressing the following nucleotide molecules being represented by nucleotide sequences, wherein the expression of these nucleotide sequences confers on the cell the ability to convert pyruvate into 2,3-butanediol and/or into butanol:

(a) a nucleotide sequence encoding a 2-acetolactate synthetase, wherein said nucleotide sequence is selected from the group consisting of:

Acetone as Organic Product

When an organic product to be produced is acetone, preferred nucleic acid molecules code for enzymes capable of converting pyruvate into acetone and/or into an intermediary compound produced in the pathway leading to acetone, said enzymes comprise a thiolase, an acetoacetylCoA transferase and an acetoacetate decarboxylase. Therefore, in this preferred embodiment, a Cyanobacterium comprises a nucleic acid molecule encoding a thiolase, an acetoacetylCoA transferase and another one encoding an acetoacetylCoA decarboxylase. Accordingy, this preferred embodiment relates to a Cyanobacterium capable of expressing the following nucleic acid molecules being represented by nucleotide sequences, wherein the expression of these nucleotide sequences confers on the cell the ability to convert pyruvate into acetone:

(a) a nucleotide sequence encoding a thiolase, wherein said nucleotide sequence is selected from the group consisting of:

1,3-Propanediol as Organic Product

When an organic product to be produced is 1,3-propanediol, preferred nucleic acid molecules code for enzymes capable of converting glyceraldehyde-3-phosphate into propanediol and/or into an intermediary compound produced in the pathway leading to 1,3-propanediol, said enzymes comprise a glycerol-3-P-dehydrogenase, a glycerol-3-P-phosphatase, a glycerol dehydratase and an oxidoreductase. A first intermediary product is glycerol. A preferred assay for glycerol is HPLC. A detectable amount of glycerol is preferably at least 0.1 mM under said culture conditions as defined earlier herein and using said assay. A second intermediary product is hydroxypronionaldehyde. A preferred assay for hydroxypropionaldehyde is HPLC. A detectable amount of hydroxypropionaldehyde is preferably at least 0.1 mM under said culture conditions as defined earlier herein and using said assay. Alternatively, a cell may produce a combination of a first and a second intermediary product as defined above. In this case, a detectable amount of a first and a second intermediary product as defined above is at least 0.1 mM of each intermediary product. Therefore in this preferred embodiment, a Cyanobacterium comprises a nucleic acid molecule encoding a glycerol-3-P-dehydrogenase, a glycerol-3-P-phosphatase, a glycerol dehydratase and an oxidoreductase. Accordingly, this preferred embodiment relates to a Cyanobacterium capable of expressing the following nucleic acid molecules being represented by nucleotide sequences, wherein the expression of these nucleotide sequences confers on the cell the ability to convert glyceraldehyde-3-phosphate into glycerol, hydroxypropionaldehyde and/or 1,3-propanediol:

(a) a nucleotide sequence encoding a glycerol-3-P-dehydrogenase, wherein said nucleotide sequence is selected from the group consisting of:

D-lactate as Organic Product

When an organic product to be produced is D-lactate, preferred nucleic acid molecules code for enzymes capable of converting pyruvate into D-lactate, said enzyme comprise a lactate dehydrogenase. Preferred assays for D-lactate are HPLC and enzymatic assays. A detectable amount by HPLC of D-lactate is preferably at least 0.1 mM under said culture conditions as defined earlier herein and using said assay. A detectable amount by enzymatic assays of D-lactate is preferably at least 0.2 mg/l under said culture conditions as defined earlier herein and using said assay. Therefore, in this preferred embodiment, a Cyanobacterium comprises a nucleic acid molecule encoding a lactate dehydrogenase. Accordingly, this preferred embodiment relates to a Cyanobacterium capable of expressing at least one nucleic acid molecule, said nucleic acid molecule being represented by a nucleotide sequence, wherein the expression of this nucleotide sequence confers on the cell the ability to convert pyruvate into D-lactate:

(a) a nucleotide sequence encoding a lactate dehydrogenase, wherein said nucleotide sequence is selected from the group consisting of:

Ethylene as Organic Product

When an organic product to be produced is ethylene, preferred nucleic acid molecules code for enzymes capable of converting 2-oxoglutarate into ethylene and succinate, said enzyme comprise a ethylene forming enzyme (2-oxoglutarate-dependent ethylene-forming enzyme). A preferred assay for ethylene is GC (gas chromatography) under said culture conditions as defined earlier herein and using said assay. As shown by (Pirkov I et al, (2008), Metabolic Engineering, 10: 276-280). A detectable amount of ethylene is preferably at least 10 μg/1 h. Therefore, in this preferred embodiment, a Cyanobacterium comprises a nucleic acid molecule encoding a ethylene forming enzyme. Accordingly, this preferred embodiment relates to a Cyanobacterium capable of expressing at least one nucleic acid molecule, said nucleic acid molecule being represented by a nucleotide sequence, wherein the expression of this nucleotide sequence confers on the cell the ability to convert 2-oxoglutarate into ethylene and succinate:

(a) a nucleotide sequence encoding a ethylene forming enzyme, wherein said nucleotide sequence is selected from the group consisting of:

Each nucleotide sequence or amino acid sequence described herein by virtue of its identity percentage (at least 40%) with a given nucleotide sequence or amino acid sequence respectively has in a further preferred embodiment an identity of at least 45%, 50%, 55%, 60%, 65%, 70%, 75%, 80%, 85%, 90%, 95%, 98%, 99% or more identity with the given nucleotide or amino acid sequence respectively. In a preferred embodiment, sequence identity is determined by comparing the whole length of the sequences as identified herein.

Each nucleotide sequence encoding an enzyme as described herein may encode either a prokaryotic or an eukaryotic enzyme, i.e. an enzyme with an amino acid sequence that is identical to that of an enzyme that naturally occurs in a prokaryotic or eukaryotic organism. The present inventors have found that the ability of a particular enzyme or to a combination of particular enzymes as defined herein to confer to a Cyanobacterial cell the ability to convert a glycolytic intermediate into an organic product and/or into an intermediary compound produced in the pathway leading to the organic compound does not depend so much on whether the enzyme is of prokaryotic or eukaryotic origin. Rather this depends on the relatedness (identity percentage) of the enzyme amino acid sequence or corresponding nucleotide sequence to that of the corresponding identified SEQ ID NO.

Alternatively or in combination with previous preferred embodiments, the invention relates to a further preferred embodiment, wherein at least one enzyme as defined herein is substantially not sensitive towards oxygen inactivation. “Being substantially not sensitive towards oxygen inactivation” preferably means that when such enzyme is expressed in a Cyanobacterium as described herein and when this Cyanobacterium is cultured in a process of the invention, significant activity of said enzyme is detectable using a specific assay known to the skilled person. More preferably, a significant activity of said enzyme is at least 20% of the activity of the same enzyme expressed in the same Cyanobacterium but cultured in the absence of oxygen. Even more preferably, at least 30%, 35%, 40%, 45%, 50%, 55%, 60%, 65%, 70%, 75%, 80%, 85%, 90%, 95% of the activity is detectable. Most preferably, the activity of said enzyme as expressed in a Cyanobacterium as described herein and when this Cyanobacterium is cultured in the process of the invention is identical with the activity of the same enzyme as expressed in a same Cyanobacterium as described herein and when this Cyanobacterium is cultured in the absence of oxygen. This is an advantage of the present invention that the Cyanobacterium hence obtained is preferably used in a process of the invention wherein oxygen is produced, since it will substantially not affect the activity of the enzymes used herein.

Alternatively or in combination with previous preferred embodiments, the invention relates to a further preferred embodiment wherein, a Cyanobacterium as defined herein is a Cyanobacterium that has been transformed with a nucleic acid construct comprising a nucleotide sequence encoding an enzyme as defined above depending on the organic product to be produced. A nucleic acid construct comprising a nucleic acid molecule coding for a given enzyme as defined herein will ensure expression of the given nucleic acid molecule, and of the corresponding enzyme in a Cyanobacterium. In a more preferred embodiment, a nucleic acid construct comprises more than one nucleic acid molecule, each nucleic acid molecule coding for a given enzyme. In an even more preferred embodiment, a nucleic acid construct comprises two, three, four nucleic acid molecules, each nucleic acid molecule coding for a given enzyme. In a most preferred embodiment, a nucleic acid construct comprises all nucleic acid molecules needed for the conversion of a glycolytic intermediate into an organic product and/or an intermediary compound, each nucleic acid molecule coding for a given enzyme. This most preferred embodiment is illustrated in example 2. In this most preferred embodiment, a nucleic acid construct comprises an expression cassette, said expression cassette comprising each needed nucleic acid molecule. Each nucleic acid molecule is operably linked with other nucleic acid molecule present. Most preferably, a suitable promoter is operably linked with the expression cassette to ensure expression of the nucleic acid molecule in a Cyanobacterium as later defined herein.

To this end, a nucleic acid construct may be constructed as described in e.g. U.S. Pat. No. 6,699,696 or U.S. Pat. No. 4,778,759. A Cyanobacterium may comprise a single but preferably comprises multiple copies of each nucleic acid construct. A nucleic acid construct may be maintained episomally and thus comprises a sequence for autonomous replication, such as an ARS sequence. Suitable episomal nucleic acid constructs may e.g. be based on the yeast 2μ or pKD1 (Fleer et al., 1991, Biotechnology 9:968-975) plasmids. Preferably, however, each nucleic acid construct is integrated in one or more copies into the genome of a cyanobacterial cell. Integration into a cyanobacterial cell's genome may occur at random by illegitimate recombination but preferably a nucleic acid construct is integrated into the Cyanobacterium cell's genome by homologous recombination as is well known in the art (U.S. Pat. No. 4,778,759). Homologous recombination occurs preferably at a neutral integration site. A neutral integration site is an integration which is not expected to be necessary for the production process of the invention, i.e for the growth and/or the production of an organic compound and/or an intermediary compound as defined herein. A preferred integration site is the nrt operon as illustrated in the examples (Osanai, T., Imamura, S., Asayama, M., Shirai, M., Suzuki, I., Murata, N., Tanaka, K, (2006) Nitrogen induction of sugar catabolic gene expression in Synechocystis sp. PCC 6803. DNA Research 13, 185-19). Accordingly, in a more preferred embodiment, a cyanobacterial cell of the invention comprises a nucleic acid construct comprising a nucleic acid molecule, said nucleic acid molecule being represented by a nucleotide sequence, said nucleotide sequence being a coding sequence of an enzyme as identified herein. Said cyanobacterial cell is capable of expression of these enzymes. In an even more preferred embodiment, a nucleic acid molecule encoding an enzyme is operably linked to a promoter that causes sufficient expression of a corresponding nucleic acid molecule in a Cyanobacterium to confer to a Cyanobacterium the ability to convert a glycolytic intermediate into a given organic product and/or into an intermediary compound produced in the pathway leading to the organic product. In case of an expression cassette as earlier defined herein, a promoter is upstream of the expression cassette. Accordingly, in a further aspect, the invention also encompasses a nucleic acid construct as earlier outlined herein. Preferably, a nucleic acid construct comprises a nucleic acid molecule encoding an enzyme as earlier defined herein. Nucleic acid molecules encoding an enzyme have been all earlier defined herein.

A promoter that could be used to achieve the expression of a nucleic acid molecule coding for an enzyme as defined herein may be not native to a nucleic acid molecule coding for an enzyme to be expressed, i.e. a promoter that is heterologous to the nucleic acid molecule (coding sequence) to which it is operably linked. Although a promoter preferably is heterologous to a coding sequence to which it is operably linked, it is also preferred that a promoter is homologous, i.e. endogenous to a Cyanobacterium. Preferably, a heterologous promoter (to the nucleotide sequence) is capable of producing a higher steady state level of a transcript comprising a coding sequence (or is capable of producing more transcript molecules, i.e. mRNA molecules, per unit of time) than is a promoter that is native to a coding sequence, preferably under conditions where sun light and carbon dioxide are present. A suitable promoter in this context includes both constitutive and inducible natural promoters as well as engineered promoters. A promoter used in a Cyanobacterium cell of the invention may be modified, if desired, to affect its control characteristics. A preferred promoter is a SigE controlled promotor of the glyceraldehyde dehydrogenase gene from Synechocystis PCC 6083 as identified in SEQ ID NO:74 (Takashi Osanai, et al, Positive Regulation of Sugar Catabolic Pathways in the Cyanobacterium Synechocystis sp. PCC 6803 by the Group 2 sigma Factor SigE. J. Biol. Chem. (2005) 35: 30653-30659). This promoter is quite advantageous to be used as outlined below in the next paragraph.

Alternatively or in combination with previous preferred embodiments, the invention relates to a further preferred embodiment, wherein the expression of a nucleic acid molecule as defined herein is regulated so as to respond to a change in the concentration of a nutrient such as ammonium (Osanai, T., Imamura, S., Asayama, M., Shirai, M., Suzuki, I., Murata, N., Tanaka, K, (2006) Nitrogen induction of sugar catabolic gene expression in Synechocystis sp. PCC 6803. DNA Research 13, 185-195). In a more preferred embodiment, the expression of a nucleic acid molecule is induced when ammonium concentration is below a given value. As exemplified in example 2, this is preferably achieved by using a SigE promoter in a nucleic acid construct comprising a nucleic acid molecule as defined herein. Such promoter is inactive in a first phase of the process when ammonium is present in a concentration which is approximately above 1 mM. In this first phase, a Cyanobacterium will grow and not produce any organic compound and/or any intermediary compound as defined herein. When the ammonium source, has been used for growth and its concentration is approximately below 1 mM, the SigE promoter is induced. As a consequence, the process is divided in 2 phase, a first phase where cell numbers increase and a second phase of the production process of the invention, which is characterized by the production of an organic compound and/or an intermediary compound as defined herein. This two phased production process has several advantages compared to one phase production processes: a) the growth phase is separated from the production phase and therefore high cell densities can be obtained in a short time b) the yield of an organic product and/or of an intermediary compound as defined herein will be improved due to the fact that no carbon flux to growth will occur in the second phase. The skilled person knows how to assess the concentration of a nutrient such as ammonium in the culture.

Method

In a second aspect, the invention relates to a process of producing an organic compound and/or an intermediary compound as defined herein by feeding carbon dioxide to a culture of a cyanobacterial cell and subjecting said culture to light, wherein said cell is capable of expressing a nucleic acid molecule, wherein the expression of said nucleic acid molecule confer on the cell the ability to convert a glycolytic intermediate into an organic compound and/or into an intermediary compound produced in the pathway leading to the organic compound and wherein said nucleic acid molecule is under the control of a regulatory system which responds to a change in the concentration of a nutrient in said culture.

A Cyanobacterium, a glycolytic intermediate, an organic compound, an intermediary compound, a nucleic acid molecule, and a regulatory system have all earlier been defined herein.

In a process of the invention, carbon dioxide is fed to a culture broth of Cyanobacteria. The skilled person knows that the carbon dioxide concentration is dependent from the temperature, the pH and the concentration of carbon dioxide present in the air used. Therefore, this is quite difficult to give an estimation of the concentration of carbon dioxide which is being used. Below, we give estimations of preferred concentrations used. A preferred feeding concentration of carbon dioxide is air enriched to 5% carbon dioxide. A preferred source of carbon dioxide may be the waste gas from an industrial plant.

Usually a process is started with a culture (also named culture broth) of Cyanobacteria having an optical density measured at 660 nm of approximately 0.2 to 2.0 (OD660=0.2 to 2) as measured in any conventional spectrophotometer with a measuring path length of 1 cm. Usually the cell number in the culture doubles every 20 hours. A preferred process takes place in a tank with a depth of 30-50 cm exposed to sun light. In a preferred process, the number of cells increases until the source of ammonium is exhausted or below a given value as earlier explained herein, subsequently the production of said products and/or intermediates will start. In a preferred embodiment, the light used is natural. A preferred natural light is sunlight. Sunlight may have an intensity ranged between approximately 1000 and approximately 1500 μEinstein/m2/s. In another preferred embodiment, the light used is artificial. Such artificial light may have an intensity ranged between approximately 70 and approximately 800 μEinstein/m2/s.

In a preferred process, an organic compound and/or an intermediate compound produced is separated from the culture broth. This may be realized continuously with the production process or subsequently to it. Separation may be based on membrane technology and/or evaporation methods. Depending on the identity of the organic compound and/or of intermediary compound produced, the skilled person will know which separating method is the most appropriate.

General Definitions

Sequence Identity and Similarity

Sequence identity is herein defined as a relationship between two or more amino acid (polypeptide or protein) sequences or two or more nucleic acid (polynucleotide) sequences, as determined by comparing the sequences. Usually, sequence identities or similarities are compared over the whole length of the sequences compared. In the art, “identity” also means the degree of sequence relatedness between amino acid or nucleic acid sequences, as the case may be, as determined by the match between strings of such sequences. “Similarity” between two amino acid sequences is determined by comparing the amino acid sequence and its conserved amino acid substitutes of one polypeptide to the sequence of a second polypeptide. “Identity” and “similarity” can be readily calculated by various methods, known to those skilled in the art. In a preferred embodiment, sequence identity is determined by comparing the whole length of the sequences as identified herein.

Preferred methods to determine identity are designed to give the largest match between the sequences tested. Methods to determine identity and similarity are codified in publicly available computer programs. Preferred computer program methods to determine identity and similarity between two sequences include e.g. the BestFit, BLASTP (Protein Basic Local Alignment Search Tool), BLASTN (Nucleotide Basic Local Alignment Search Tool), and FASTA (Altschul, S. F. et al., J. Mol. Biol. 215:403-410 (1990), publicly available from NCBI and other sources (BLAST Manual, Altschul, S., et al., NCBI NLM NIH Bethesda, MD 20894). A most preferred algorithm used is EMBOSS (European Molecular Biology Open Software Suite).

Preferred parameters for amino acid sequences comparison using EMBOSS are gap open 10.0, gap extend 0.5, Blosum 62 matrix. Preferred parameters for nucleic acid sequences comparison using EMBOSS are gap open 10.0, gap extend 0.5, DNA full matrix (DNA identity matrix).

Optionally, in determining the degree of amino acid similarity, the skilled person may also take into account so-called “conservative” amino acid substitutions, as will be clear to the skilled person. Conservative amino acid substitutions refer to the interchangeability of residues having similar side chains. For example, a group of amino acids having aliphatic side chains is glycine, alanine, valine, leucine, and isoleucine; a group of amino acids having aliphatic-hydroxyl side chains is serine and threonine; a group of amino acids having amide-containing side chains is asparagine and glutamine; a group of amino acids having aromatic side chains is phenylalanine, tyrosine, and tryptophan; a group of amino acids having basic side chains is lysine, arginine, and histidine; and a group of amino acids having sulphur-containing side chains is cysteine and methionine. Preferred conservative amino acids substitution groups are: valine-leucine-isoleucine, phenylalanine-tyrosine, lysine-arginine, alanine-valine, and asparagine-glutamine. Substitutional variants of the amino acid sequence disclosed herein are those in which at least one residue in the disclosed sequences has been removed and a different residue inserted in its place. Preferably, the amino acid change is conservative. Preferred conservative substitutions for each of the naturally occurring amino acids are as follows: Ala to ser; Arg to lys; Asn to gln or his; Asp to glu; Cys to ser or ala; Gln to asn; Glu to asp; Gly to pro; His to asn or gln; Ile to leu or val; Leu to ile or val; Lys to arg; gln or glu; Met to leu or ile; Phe to met, leu or tyr; Ser to thr; Thr to ser; Trp to tyr; Tyr to trp or phe; and, Val to ile or leu.

Hybridising Nucleic Acid Sequences

Nucleotide sequences encoding the enzymes expressed in the cell of the invention may also be defined by their capability to hybridise with the nucleotide sequences of SEQ ID NO: 2, 4, 6, 8, 16, 18, 20, 22, 24, 26, 28, 30, 32, 34, 36, 76, 78, 80, 82, 86, 87, 88, 90, 92, 96 respectively, under moderate, or preferably under stringent hybridisation conditions. Stringent hybridisation conditions are herein defined as conditions that allow a nucleic acid sequence of at least about 25, preferably about 50 nucleotides, 75 or 100 and most preferably of about 200 or more nucleotides, to hybridise at a temperature of about 65° C. in a solution comprising about 1 M salt, preferably 6 × SSC or any other solution having a comparable ionic strength, and washing at 65° C. in a solution comprising about 0.1M salt, or less, preferably 0.2 × SSC or any other solution having a comparable ionic strength. Preferably, the hybridisation is performed overnight, i.e. at least for 10 hours and preferably washing is performed for at least one hour with at least two changes of the washing solution. These conditions will usually allow the specific hybridisation of sequences having about 90% or more sequence identity.

Moderate conditions are herein defined as conditions that allow a nucleic acid sequences of at least 50 nucleotides, preferably of about 200 or more nucleotides, to hybridise at a temperature of about 45° C. in a solution comprising about 1 M salt, preferably 6×SSC or any other solution having a comparable ionic strength, and washing at room temperature in a solution comprising about 1 M salt, preferably 6×SSC or any other solution having a comparable ionic strength. Preferably, the hybridisation is performed overnight, i.e. at least for 10 hours, and preferably washing is performed for at least one hour with at least two changes of the washing solution. These conditions will usually allow the specific hybridisation of sequences having up to 50% sequence identity. The person skilled in the art will be able to modify these hybridisation conditions in order to specifically identify sequences varying in identity between 50% and 90%.

Homologous

The term “homologous” when used to indicate the relation between a given (recombinant) nucleic acid or polypeptide molecule and a given host organism or host cell, is understood to mean that in nature the nucleic acid or polypeptide molecule is produced by a host cell or organisms of the same species, preferably of the same variety or strain. If homologous to a host cell, a nucleic acid sequence encoding a polypeptide will typically be operably linked to another promoter sequence than in its natural environment. When used to indicate the relatedness of two nucleic acid sequences the term “homologous” means that one single-stranded nucleic acid sequence may hybridize to a complementary single-stranded nucleic acid sequence. The degree of hybridization may depend on a number of factors including the amount of identity between the sequences and the hybridization conditions such as temperature and salt concentration as earlier presented. Preferably the region of identity is greater than about 5 bp, more preferably the region of identity is greater than 10 bp. Preferably, two nucleic acid or polypeptides sequences are said to be homologous when they have more than 80% identity.

Heterologous

The term “heterologous” when used with respect to a nucleic acid (DNA or RNA) or protein refers to a nucleic acid or protein (also named polypeptide or enzyme) that does not occur naturally as part of the organism, cell, genome or DNA or RNA sequence in which it is present, or that is found in a cell or location or locations in the genome or DNA or RNA sequence that differ from that in which it is found in nature. Heterologous nucleic acids or proteins are not endogenous to the cell into which it is introduced, but has been obtained from another cell or synthetically or recombinantly produced. Generally, though not necessarily, such nucleic acids encode proteins that are not normally produced by the cell in which the DNA is transcribed or expressed. Similarly exogenous RNA encodes for proteins not normally expressed in the cell in which the exogenous RNA is present. Heterologous nucleic acids and proteins may also be referred to as foreign nucleic acids or proteins. Any nucleic acid or protein that one of skill in the art would recognize as heterologous or foreign to the cell in which it is expressed is herein encompassed by the term heterologous nucleic acid or protein. The term heterologous also applies to non-natural combinations of nucleic acid or amino acid sequences, i.e. combinations where at least two of the combined sequences are foreign with respect to each other.

Operably Linked

As used herein, the term “operably linked” refers to a linkage of polynucleotide elements (or coding sequences or nucleic acid sequence or nucleic acid molecule) in a functional relationship. A nucleic acid sequence is “operably linked” when it is placed into a functional relationship with another nucleic acid sequence. For instance, a promoter or enhancer is operably linked to a coding sequence if it affects the transcription of the coding sequence. Operably linked means that the nucleic acid sequences being linked are typically contiguous and, where necessary to join two protein coding regions, contiguous and in reading frame.

Promoter

As used herein, the term “promoter” refers to a nucleic acid fragment that functions to control the transcription of one or more nucleic acid molecules, located upstream with respect to the direction of transcription of the transcription initiation site of the nucleic acid molecule, and is structurally identified by the presence of a binding site for DNA-dependent RNA polymerase, transcription initiation sites and any other DNA sequences, including, but not limited to transcription factor binding sites, repressor and activator protein binding sites, and any other sequences of nucleotides known to one of skill in the art to act directly or indirectly to regulate the amount of transcription from the promoter. A “constitutive” promoter is a promoter that is active under most environmental and developmental conditions. An “inducible” promoter is a promoter that is active under environmental or developmental regulation.

Genetic Modifications

For overexpression of an enzyme in a host cells=of the inventions as described above, as well as for additional genetic modification of a host cell=, preferably Cyanobacteria, host cells are transformed with the various nucleic acid constructs of the invention by methods well known in the art. Such methods are e.g. known from standard handbooks, such as Sambrook and Russel (2001) “Molecular Cloning: A Laboratory Manual (3rd edition), Cold Spring Harbor Laboratory, Cold Spring Harbor Laboratory Press, or F. Ausubel et al, eds., “Current protocols in molecular biology”, Green Publishing and Wiley Interscience, New York (1987). Methods for transformation and genetic modification of cyanobacterial cells are known from e.g. U.S. Pat. No. 6,699,696 or U.S. Pat. No. 4,778,759.

A promoter for use in a nucleic acid construct for overexpression of an enzyme in a cyanobacterial cell of the invention has been described above. Optionally, a selectable marker may be present in a nucleic acid construct. As used herein, the term “marker” refers to a gene encoding a trait or a phenotype which permits the selection of, or the screening for, a Cyanobacterial cell containing the marker. A marker gene may be an antibiotic resistance gene whereby the appropriate antibiotic can be used to select for transformed cells from among cells that are not transformed. Preferably however, a non-antibiotic resistance marker is used, such as an auxotrophic marker (URA3, TRP1, LEU2). In a preferred embodiment, a Cyanobacterial cell transformed with a nucleic acid construct is marker gene free. Methods for constructing recombinant marker gene free microbial host cells are disclosed in EP-A-0 635 574 and are based on the use of bidirectional markers. Alternatively, a screenable marker such as Green Fluorescent Protein, lacZ, luciferase, chloramphenicol acetyltransferase, beta-glucuronidase may be incorporated into a nucleic acid construct of the invention allowing to screen for transformed cells.

Optional further elements that may be present in a nucleic acid construct of the invention include, but are not limited to, one or more leader sequences, enhancers, integration factors, and/or reporter genes, intron sequences, centromers, telomers and/or matrix attachment (MAR) sequences. A nucleic acid construct of the invention can be provided in a manner known per se, which generally involves techniques such as restricting and linking nucleic acids/nucleic acid sequences, for which reference is made to the standard handbooks, such as Sambrook and Russel (2001) “Molecular Cloning: A Laboratory Manual (3rd edition), Cold Spring Harbor Laboratory, Cold Spring Harbor Laboratory Press.

Methods for inactivation and gene disruption in Cyanobacterial cells are well known in the art (see e.g. Shestakov S V et al, (2002), Photosynthesis Research, 73: 279-284 and Nakamura Y et al, (1999), Nucleic Acids Res. 27:66-68).

In this document and in its claims, the verb “to comprise” and its conjugations is used in its non-limiting sense to mean that items following the word are included, but items not specifically mentioned are not excluded. In addition the verb “to consist” may be replaced by “to consist essentially of” meaning that a peptide or a composition as defined herein may comprise additional component(s) than the ones specifically identified, said additional component(s) not altering the unique characteristic of the invention. In addition, reference to an element by the indefinite article “a” or “an” does not exclude the possibility that more than one of the element is present, unless the context clearly requires that there be one and only one of the elements. The indefinite article “a” or “an” thus usually means “at least one”.

All patent and literature references cited in the present specification are hereby incorporated by reference in their entirety. The following examples are offered for illustrative purposes only, and are not intended to limit the scope of the present invention in any way

FIG. 1: The light reaction reproduced from Berg, Tymoczko and Stryer: “Biochemistry” WH Freeman and Co, New York, 2006.

FIG. 2: The Calvin Cycle reproduced from Berg, Tymoczko and Stryer: “Biochemistry” WH Freeman and Co, New York, 12006.

FIG. 3: Construction of a recombinant strain: The cassette is introduced by homologous recombination and positioned downstream the SigE controlled promotor of Synechocystis PCC 6803. The black circle shows the suicide plasmid (e.g. pBluescript) that is not able to replicate in Synechocystis PCC 6803. The cassette(s) of interest (denoted as arrow “x” in the figure) will be engineered to be flanked by DNA sequences homologous to a non-coding DNA region (shown as a dotted bar in the figure) in the nrt operon. Via a double crossover event, shown in the figure as dashed crosses, the cassettes of interest are integrated into the Synechocystis genome. Alternatively, the construct can be inserted at a neutral docking site.

FIG. 4: Ammonium controlled production via the NtcA transcriptional regulator. Conditions allowing growth repress production, ammonium depletion promotes production.

FIG. 5: Alcohol resistance. After five days, 100 μA of each culture was diluted and transferred to solid medium prepared from the BG-11 medium. Solid cultures were grown in an incubator at 30° C. under continuous illumination (70 μEinstein/m2/s) using two TL tubes without any addition (control) or with butanol, respectively ethanol added at various concentrations. After a week, single colonies were observed and counted. The amount of colonies was compared to the control sample.

The energy, in the form of ATP, as well as the reductive power in the form of NADPH, that are both needed to drive the subsequent highly endergonic dark reactions of photosynthesis, are catalyzed by the two photosystems of oxygenic photosynthesis, PS -II and PS-I, arranged according to the well-known Z-scheme, plus the membrane -bound ATPase (FIG. 1).

In phototrophic organisms like Cyanobacteria, CO2 is fixed in the so-called Calvin cycle. This is a cyclic series of reductive steps that result in the net conversion of CO2 into C3 compounds, such as glyceraldehyde-3-phosphate, phosphoglycerate and pyruvate (FIG. 2).

This pathway is essentially endergonic and in Nature driven by sunlight. It consumes CO2 and water and yields C3 compounds (e.g. pyruvate) and oxygen:
CO2+H2O+Solar energy→C3 compounds+O2  (1)

This reaction cannot proceed spontaneously: It is driven by the consumption of the ATP and NADPH, generated in the ‘light’ reactions of photosynthesis. Subsequently, the C3 compounds are used in Nature (i.e. in phototrophic organisms like plants and Cyanobacteria) as the building blocks to make new cells and/or plants. This requires additional amounts of reducing power (as NADPH) and energy conserved during the light capturing reactions (as ATP) and also allows the organisms to proliferate (grow and survive).

Nature also sustains an entirely different mode of (microbial) life: Numerous bacterial and fungal species are able to conserve sufficient energy (as ATP) to proliferate by fermentation, in which they use so-called substrate level phosphorylation to generate their energy. This respiration-independent mode of energy conservation relies on metabolic pathways that result in redox neutral dissimilation of the energy source. The most abundant pathways have evolved with sugars (e.g. glucose) as energy source and therefore all have glycolysis in common:
Glucose→glyceraldehyde-P→pyruvate+reducing power  (2)

Redox neutrality is maintained by the generalized reaction:
pyruvate+reducing power→fermentation products  (3)

Thus, it will contain the functional biochemistry to reduce the above-mentioned intermediates to the end product and will have as its biocatalytic input and output the combination of (1) and (3), respectively:
CO2+H2O+Solar energy→organic product+O2

Genetic Cassettes

The identity of an organic product formed (and excreted into the environment) in the process of the invention depends on the species-specific gene cassettes (i.e. nucleic acid molecules represented by nucleotide sequences) that encode the respective biochemical pathway (see table 1). Preferred enzymes encoded by nucleic acid molecules are substantially oxygen insensitive.

TABLE 1
Examples of preferred donor organisms for the nucleic acid molecules or genes to be
introduced into a Cyanobacterium with the pathway they catalyze. For e.g. the production
of ethanol and propanediol various alternative donor organisms can be suggested.
donor genes pathway
Sarcina ventriculi pyruvate decarboxylase, Pyruvate → acetaldehyde
Lactobacillus brevis alcohol dehydrogenase Acetaldehyde → ethanol
Clostridium thiolase pyruvate acetoacetylCoA
acetobutilicum hydroxybutyrylCoA
dehydrogenase acetoacetylCoA → butyrylCoA
crotonase
butyryl-CoA dehydrogenase butyrylCoA → butyraldehyde
Butanol dehydrogenase butyraldehyde → 2-butanol
Pseudomonas syringiae ethylene forming enzyme 2-ketoglutarate → ethylene
Lactococcus lactis lactate dehydrogenase pyruvate → D-lactate
Lactococcus lactis acetolactate synthase pyruvate → 2-acetolactate
acetolactate decarboxylase 2-acetolactate → acetoin
diacetyl reductase diacetyl → acetoin
acetoin reductase acetoin → 2,3 butanediol
Klebsiella pneumoniae glycerol dehydratase 2,3 butanediol → 2-butanone
1,3 propanediol 2-butanone → 2-butanol
dehydrogenase
Clostridium thiolase acetylCoA → acetoacetylCoA
acetobutilicum ac.acetylCoA transferase acetoacetylCoA → acetoacetate
acetoacetate decarboxylase acetoacetate → acetone
Clostridium thiolase acetylCoA → acetoacetylCoA
acetobutilicum ac.acetylCoA transferase acetoacetylCoA → acetoacetate
acetoacetate decarboxylase acetoacetate → acetone
Klebsiella pneumoniae propanol dehydrogenase acetone → propanol
Synechocystis PCC glycerol-3-P dehydrogenase GAP → glycerol-P
6083 glycerol-3-P Phosphatase glycerol-P → glycerol
K. pneumoniae glycerol dehydratase glycerol → OHpropionaldehyde
oxidoreductase OHprop.aldehyde → 1,3-propanediol

A preferred design of expression cassettes is given in table 2.

TABLE 2
design of expression cassettes
Product donor strain Cassette Pathway
Ethanol Sarcina ventriculi Lactobacillus brevis ##STR00001## pyruvate acetaldehyde pdc adh 1 ethanol
Acetone Clostridium acetobutylicum ##STR00002## Ac-CoA thl acetoacylCoA ctfAB Ac.acetate adc acetone
Propanol Clostridium acetobutylicum Klebsiella pneumoniae ##STR00003## acetone aad propanol
Ethylene Pseudomonas syringiae ##STR00004## 2-ketoglutarate efe ethylene
Butanol Clostridium acetobutylicum ##STR00005## etf crt 3 hbd butyrylCoA ald butyraldehyde bdh butanol
Butanol Lactococcus lactis Klebsiella pneumonia ##STR00006## pyruvate als 2-acetolactate aldb acetoin butb 2,3 butanediol dhaB 2-butanone dhaT 2-butanol
Lactic acid Lactococcus lactis ##STR00007## pyruvate ldh lactic acid
1,3 Propanediol Synechocystis sp. PCC6803 Saccharomyces cerevisiae Klebsiella pneumonia ##STR00008## glyceraldehyde-P gpd 1 glycerol-P gpp 1 glycerol dha hydroxypropionaldehyde ygd 1,3 propanediol

Homologous Integration and Ammonium Controlled Expression

The genes/cassettes, necessary for the different pathways and respective organic products in Synechocystis, are preferably introduced to Synechocystis via chromosomal integration. This will be achieved by homologous recombination which allows to precisely define the chromosomal site of insertion. Appropriate plasmids for this purpose known to be applicable in Synechocystis sp PCC 6830 are pBluescript (Stratagene, USA) or pGEM-T (Promega, USA). A strategy with respect to the construct is exemplified in FIG. 3 but alternative (neutral) docking sites for integration will be considered.

We will make use of the fact that expression of a number of glycolytic genes of Synechocystis are under control of a group 2 sigma-factor, σE. In turn, expression of the gene encoding this factor, SigE, is switched on by the transcriptional regulator NtcA1,3. This switch is, amongst other unidentified signals, dependent on the extracellular nitrogen availability via the intracellular α-oxoglutarate/glutamate ratio: under conditions of ammonium depletion of the medium to less than 1 mM2, NtcA binds to α-oxoglutarate and the resulting NtcA-α-oxoglutarate complex has a high binding affinity for and positive control on the SigE promotor. Thus, a gene cassette under SigE control will be expressed upon ammonium depletion. As a consequence, during ammonium excess conditions, the carbon flux will be directed towards biosynthesis whereas in the stationary phase this flux will be directed to production (see FIG. 4). For Synechococcus the external ammonium threshold for the switch to σE synthesis was found to be submillimolar range2.

Synechocystis PCC 6803 strain was grown on BG-11 medium (Stanier R Y, et al. Purification and properties of unicellular blue-green algae (order Chroococcales). Bacteriol. Rev. (1971) 35:171-205) in an orbital shaker at 30° C. under continuous illumination using two TL tubes, which provided average light intensity of approximately 70 μE·m−2·s−1. To quantify the influence of alcohols on the net growth rate, cells were grown without any addition (control) or with butanol, respectively ethanol added at various concentrations.

After 5 days, 100 μl of each culture was appropriately diluted and transferred to solid medium prepared from BG-11 and supplemented with 0.3% sodium thiosulfate, 10 mM N-tris[hydroxymethyl]-2-aminoethanesulfonic acid (TES) pH 8.2, 5 mM glucose and 1.5% bactoagar. Solid cultures were grown in an incubator 30° C. under continuous illumination. After a week, single colonies were observed and counted. The amount of colonies was compared to the control sample.

From the results shown below in FIG. 5, it is concluded that the net specific growth rate decreases linearly with increasing alcohol concentration and that the growth rate is reduced by 50% at concentrations of approximately 0.17 M butanol respectively 0.29 M ethanol. Therefore, it is to be expected that the two phases production process of the invention is much more efficient than a single phase production process.

TABLE 3 
list of all primers used
SEQ ID NO:
HOMOLOGY REGION 1
Forward AAAT GGTACC GAA CTG AGA TTA GCC CCG GAC KpnI  37
Reverse AAAT CTCGAG ACC AGG ACA TCC GAC TTG C XhoI  38
HOMOLOGY REGION 2
Forward CACG ACTAGT GTG ACC GGG TCA TTT TTT TGCT ATT SpeI  39
TAT TCC
Reverse AAAT TCTAGA TAA CTG CGG TAG CAC TAA AGC CGC XbaI  40
TGCCTTAG
Product: Lactic acid
Forward ldh CAAT CTCGAG ATG GCT GAT AAA CAA CGT AAG XhoI  41
Reverse ldh CAAT GAATTC TTA GTT TTT AAC TGC AGA AGC AAA TTC EcoRI  42
Product: Ethanol
Forward pdc ATAA CTCGAG GAC AAT AGG TGC TTT AAT CAC XhoI  43
Reverse pdc CGAC GATATC AGG TGT AAA ATA CCA TTT ATT AAA EcoRV  44
ATA G
Forward adh CATT GATATC ATG TCT AAC CGT TTG GAT GG EcoRV  45
Reverse adh CATA CTGCAG CTA TTG AGC AGT GTA GCC AC PstI  46
Product: 1,3-Propanediol
Forward gpd AAAT CTCGAG TCAGTGGAGACAATAGTCG XhoI  47
Reverse gpd AAAT ATCGAT ATGCGTAATTTCCCAGAAATC ClaI  48
Forward dhak CATA AAGCTT ATGAAATTCTATACTTCAACGACAG  HindIII  49
Reverse dhak AAAT GATATC TTACCAGGCGAAAGCTC EcoRV  50
Forward AAAT ATCGAT TTATTCAATGGTGTCAGGCTG ClaI  51
Gl dehydr
Reverse CCAA AAGCTT ATGAAAAGATCAAAACGATTTG HindIII  52
Gl dehydr
Forward  GGGT GATATC TTAAGGTAAAGTAAAGTCAACCCAC EcoRV  53
oxidoreductase
Reverse  AAAT GAATTC ATGTTAAACGGCCTGAAAC EcoRI  54
oxidoreductase
Lactic acid-II set of primers
Forward AAAT GGTACC GAA CTG AGA TTA GCC CCG GAC KpnI  55
HomologyI
Reverse GTTG TTT ATC AGC CAT ACCA GGA CAT CCG ACTTG  56
HomologyI
Reverse CTGCGTGCAATCCATCTTGTTCAATCAT  57
for ldh TTAGTTTTTAACTGCAGAAGCAAATTC
+Reverse GCAAAAAAATGACCCGGTCAC TCAGAAGAACTCGTCAAGAAGG  58
for KAN
Reverse for  AAAT TCTAGA TAA CTG CGG TAG CAC TAA AGC CGC XbaI  59
HomologyII TGCCTTAC
Ethanol-II set of primers
Forward AAAT GGTACC GAA CTG AGA TTA GCC CCG GAC KpnI  60
HomologyI
Reverse GATTAAAGCACCTATTGTC ACCAGGACATCCGACTTG  61
HomologyII
Reverse pdc CTACCTTACCATCCAAACGGTTAGACAT  62
AGGTGTAAAATACCATTTATTAAAATAG
Reverse adh CAATCCATCTTGTTCAATCAT   63
CTATTGAGCAGTGTAGCCACCGTC
Reverse KAN GCAAAAAAATGACCCGGTCAC   64
TCAGAAGAACTCGTCAAGAAGG
Reverse  AAAT TCTAGA TAA CTG CGG TAG CAC TAA AGC CGC XbaI  65
HomologyII TGCCTTAC
1,3-Propanediol
Forward AAAT GGTACC GAA CTG AGA TTA GCC CCG GAC KpnI  66
HomologyI
Reverse TATTGTCTCCACTGA ACCAGGACATCCGACTTG  67
HomologyI
Reverse dhg CTGTCGTTGAAGTATAGAATTTCAT  68
ATGCGTAATTTCCCAGAAATCCAAAATACG
Reverse GGTTCAGCCTGACACCATTGAATAAT  69
dha k TACCAGGCGAAAGCTCCAGTTGGAGC
Reverse GTGGTTGACTTTACTTTACCTTAA  70
glycerol ATGAAAAGATCAAAACGATTTGCAGTACTGG
dehydrts
Reverse  CAATCCATCTTGTTCAATCAT ATGTTAAACGGCCTGAAACC  71
oxidored
Reverse KAN GCAAAAAAATGACCCGGTCAC TCAGAAGAACTCGTCAAGAAGG  72
Reverse AAAT TCTAGA TAA CTG CGG TAG CAC TAA AGC CGC XbaI  73
HomologyII TGCCTTAC
Ethylene
Forward Efe TAAAGTCGACAAGGAGACTAGCATGACCAAC SalI 135
Reverse Efe TAAA GAATTC TTAGGAGCCGGTGG EcoRI  94
2-Butanol (Clostridium)
forward thl AAGGAGATTCCA ATGAGAGATGTAGTAATAGTAAG  99
reverse thl TTAGTCTCTTTCAACTACGAGAGCTGTTCCCTG 100
forward 3bdh AAGGAGATTCCA ATGAAAAAGGTATGTGTTATAG  101
reverse 3bdh TTATTTTGAATAATCGTAGAAACCTTTTCCTG  102
forward crt-etf AAGGAGATTCCA ATGTCAAAAGAGATTTATGAATCAG  103
reverse crt-etf CTACAATTTTTTTACCAAATTCAAAAACATTCC 104
forward ald AAGGAGATTCCA ATGGATTTTAATTTAACAAGAG  105
reverse ald TTATCTAAAAATTTTCCTGAAATAACTAATTTTCTGAACTTC 106
forward bdh AAGGAGATTCCA ATGCTAAGTTTTGATTATTCAATAC  107
reverse bdh TTAATATGATTTTTTAAATATCTCAAGAAGCATCCTCTG 108
2-Butanol (L.lactis and K.pneumoniae)
Foreward L. AAGGAG ACTACT ATGTCTGAGAAACAATTTGGGGC 109
lactis als
Reverse L. TCAGTAAAATTCTTCTGGCAAT 110
lactis als
Foreward L. AAGGAG ACTACT ATGTCAGAAATCACACAACTTTTTCA 111
lactis aldB
Reverse L. TCATTCAGCTACATCAATATCTTTTTTCAAAGC 112
lactis aldB
Foreward L. AAGGAG ACTACT ATGTCTAAAGTTGCAGCAGTTACTGG  113
lactis butA
Reverse L. TTAATGAAATTGCATTCCACCATC 114
lactis butA
Foreward L. AAGGAG ACTACT GTGGCTTGGTGTGGAATCTGT 115
lactis butB
Reverse L. TTATAGACCTTTTCCAGTTGGTG 116
lactis butB
Foreward K. AAGGAG ACTACT ATGAAAAGATCAAAACGATTTGCAG 117
pneumoniae dhaB
Reverse K. TCAGAATGCCTGGCGGAAAAT 118
pneumoniae dhaB
Foreward K. AAGGAG ACTACT ATGAGCTATCGTATGTTTGATTATCTGG 119
pneumoniae dhaT
Reverse K. TCAGAATGCCTGGCGGAAAAT 120
pneumoniae dhaT
Acetone
Foreward thl AAGGAGA TTCCA ATGAGAGATGTAGTAATAGTAAG 121
Reverse thl TTAGTCTCTTTCAACTACGAGAGCTGTTCCCTG 122
Foreward ctfAB AAGGAG GCGGCG ATGAACTCTAAAATAATTAG 123
Reverse ctfAB TTATGCAGGCTCCTTTACTATATAAT 124
Foreward adc AAGGAG GCGGCG ATGTTAAAGGATGAAGTA 125
Reverse adc CCCTTACTTAAGATAATCATATATAA CTTCAGC 126
Propanol
Foreward thl AAGGAGA TTCCA ATGAGAGATGTAGTAATAGTAAG 127
Reverse thl TTAGTCTCTTTCAACTACGAGAG CTGTTCCCTG 128
Foreward ctfAB AAGGAG GCGGCG ATGAACTCTAAAATAATTAG 129
Reverse ctfAB TTATGCAGGCTCCTTTACTATATAAT 130
Foreward adc AAGGAG GCGGCG ATGTTAAAGGATGAAGTA 131
Reverse adc CCCTTACTTAAGATAATCATATATAACTTCAGC 132
Foreward K. AAGGAGAATTCCAATGCATACCTTTTCTCTGC 133
pneumoniae aad
Reverse K. TCATTGCAGGTTCTCCAGCAGTTGC 134
pneumoniae aad

References

Teixeira De Mattos, Maarten Joost, Hellingwerf, Klaas Jan

Patent Priority Assignee Title
Patent Priority Assignee Title
4778759, Jul 09 1982 Boyce, Thompson Institute for Plant Research, Inc. Genetic engineering in cyanobacteria
6699696, Feb 19 1997 ALGENOL BIOFUELS CANADA INC Genetically modified cyanobacteria for the production of ethanol, the constructs and method thereof
7682821, Nov 02 2006 Algenol Biofuels Switzerland GmbH Closed photobioreactor system for continued daily in situ production, separation, collection, and removal of ethanol from genetically enhanced photosynthetic organisms
8349587, Oct 31 2011 GINKGO BIOWORKS, INC Methods and systems for chemoautotrophic production of organic compounds
8669094, Jun 05 2008 GEVO, INC Enhanced pyruvate to acetolactate conversion in yeast
8735651, Feb 23 2008 Designer organisms for photobiological butanol production from carbon dioxide and water
20070072279,
20090104656,
EP635574,
EP1731604,
FR2862660,
FR2864967,
WO2007041269,
WO2007084477,
WO2007130518,
WO2008137404,
WO9821341,
WO9839457,
WO9914335,
WO9928480,
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